JP2015221041A - Whey protein product and preparation method therefor - Google Patents
Whey protein product and preparation method therefor Download PDFInfo
- Publication number
- JP2015221041A JP2015221041A JP2015132362A JP2015132362A JP2015221041A JP 2015221041 A JP2015221041 A JP 2015221041A JP 2015132362 A JP2015132362 A JP 2015132362A JP 2015132362 A JP2015132362 A JP 2015132362A JP 2015221041 A JP2015221041 A JP 2015221041A
- Authority
- JP
- Japan
- Prior art keywords
- whey protein
- product
- protein product
- milk
- casein
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 108010046377 Whey Proteins Proteins 0.000 title claims abstract description 136
- 102000007544 Whey Proteins Human genes 0.000 title claims abstract description 134
- 235000021119 whey protein Nutrition 0.000 title claims abstract description 126
- 238000002360 preparation method Methods 0.000 title claims abstract description 12
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- 235000013336 milk Nutrition 0.000 claims abstract description 56
- 239000008267 milk Substances 0.000 claims abstract description 56
- 210000004080 milk Anatomy 0.000 claims abstract description 56
- 239000005018 casein Substances 0.000 claims abstract description 35
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 claims abstract description 35
- 235000021240 caseins Nutrition 0.000 claims abstract description 35
- 102000004407 Lactalbumin Human genes 0.000 claims abstract description 13
- 108090000942 Lactalbumin Proteins 0.000 claims abstract description 13
- 235000021241 α-lactalbumin Nutrition 0.000 claims abstract description 13
- 239000000047 product Substances 0.000 claims description 141
- 239000012465 retentate Substances 0.000 claims description 47
- 238000000108 ultra-filtration Methods 0.000 claims description 46
- 238000001471 micro-filtration Methods 0.000 claims description 44
- 239000012466 permeate Substances 0.000 claims description 40
- 238000000034 method Methods 0.000 claims description 38
- 238000001728 nano-filtration Methods 0.000 claims description 37
- 108010076119 Caseins Proteins 0.000 claims description 34
- 239000008101 lactose Substances 0.000 claims description 23
- GUBGYTABKSRVRQ-QKKXKWKRSA-N Lactose Natural products OC[C@H]1O[C@@H](O[C@H]2[C@H](O)[C@@H](O)C(O)O[C@@H]2CO)[C@H](O)[C@@H](O)[C@H]1O GUBGYTABKSRVRQ-QKKXKWKRSA-N 0.000 claims description 22
- 238000010438 heat treatment Methods 0.000 claims description 16
- 238000001223 reverse osmosis Methods 0.000 claims description 15
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 14
- 239000011707 mineral Substances 0.000 claims description 14
- 235000016709 nutrition Nutrition 0.000 claims description 14
- 235000020183 skimmed milk Nutrition 0.000 claims description 12
- 235000013361 beverage Nutrition 0.000 claims description 11
- 235000013365 dairy product Nutrition 0.000 claims description 11
- 102000008192 Lactoglobulins Human genes 0.000 claims description 10
- 108010060630 Lactoglobulins Proteins 0.000 claims description 10
- 239000005862 Whey Substances 0.000 claims description 10
- 239000012141 concentrate Substances 0.000 claims description 10
- 238000011026 diafiltration Methods 0.000 claims description 10
- 235000013305 food Nutrition 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 8
- 239000002994 raw material Substances 0.000 claims description 8
- 241001465754 Metazoa Species 0.000 claims description 7
- 239000003814 drug Substances 0.000 claims description 6
- 235000012041 food component Nutrition 0.000 claims description 6
- 108010067454 caseinomacropeptide Proteins 0.000 claims description 5
- 235000021262 sour milk Nutrition 0.000 claims description 5
- 239000006071 cream Substances 0.000 claims description 4
- 235000015872 dietary supplement Nutrition 0.000 claims description 4
- 239000005417 food ingredient Substances 0.000 claims description 4
- 235000013402 health food Nutrition 0.000 claims description 4
- 235000020124 milk-based beverage Nutrition 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- 235000013376 functional food Nutrition 0.000 claims description 3
- 239000002207 metabolite Substances 0.000 claims description 3
- 230000000153 supplemental effect Effects 0.000 claims description 3
- 235000015155 buttermilk Nutrition 0.000 claims description 2
- 235000015140 cultured milk Nutrition 0.000 claims description 2
- 235000015142 cultured sour cream Nutrition 0.000 claims description 2
- 235000015141 kefir Nutrition 0.000 claims description 2
- 235000013618 yogurt Nutrition 0.000 claims description 2
- 230000002378 acidificating effect Effects 0.000 claims 2
- 239000000796 flavoring agent Substances 0.000 abstract description 18
- 235000019634 flavors Nutrition 0.000 abstract description 17
- 239000012528 membrane Substances 0.000 abstract description 14
- 235000018102 proteins Nutrition 0.000 abstract description 8
- 102000004169 proteins and genes Human genes 0.000 abstract description 8
- 108090000623 proteins and genes Proteins 0.000 abstract description 8
- 238000005516 engineering process Methods 0.000 abstract description 5
- 235000015097 nutrients Nutrition 0.000 abstract 1
- 102000011632 Caseins Human genes 0.000 description 23
- 239000000203 mixture Substances 0.000 description 11
- 230000001953 sensory effect Effects 0.000 description 11
- 235000010755 mineral Nutrition 0.000 description 10
- 239000004615 ingredient Substances 0.000 description 8
- 230000007847 structural defect Effects 0.000 description 7
- 230000008569 process Effects 0.000 description 6
- 235000000346 sugar Nutrition 0.000 description 6
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 5
- 230000009286 beneficial effect Effects 0.000 description 5
- 229960005069 calcium Drugs 0.000 description 5
- 239000011575 calcium Substances 0.000 description 5
- 229910052791 calcium Inorganic materials 0.000 description 5
- 235000001465 calcium Nutrition 0.000 description 5
- 235000013351 cheese Nutrition 0.000 description 5
- 239000003925 fat Substances 0.000 description 4
- 230000007062 hydrolysis Effects 0.000 description 4
- 238000006460 hydrolysis reaction Methods 0.000 description 4
- 238000005374 membrane filtration Methods 0.000 description 4
- 238000009928 pasteurization Methods 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 150000008163 sugars Chemical class 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000001914 filtration Methods 0.000 description 3
- 235000020190 lactose-free milk Nutrition 0.000 description 3
- 235000020121 low-fat milk Nutrition 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 239000007858 starting material Substances 0.000 description 3
- 241000283690 Bos taurus Species 0.000 description 2
- 241000283707 Capra Species 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- 241001494479 Pecora Species 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 235000019197 fats Nutrition 0.000 description 2
- 235000003599 food sweetener Nutrition 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000035764 nutrition Effects 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 235000008476 powdered milk Nutrition 0.000 description 2
- 239000003765 sweetening agent Substances 0.000 description 2
- 235000019640 taste Nutrition 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- 235000008939 whole milk Nutrition 0.000 description 2
- 241000282832 Camelidae Species 0.000 description 1
- 241000282836 Camelus dromedarius Species 0.000 description 1
- 241000283086 Equidae Species 0.000 description 1
- 241000283073 Equus caballus Species 0.000 description 1
- 241000124008 Mammalia Species 0.000 description 1
- 208000001145 Metabolic Syndrome Diseases 0.000 description 1
- 239000006057 Non-nutritive feed additive Substances 0.000 description 1
- 102000035195 Peptidases Human genes 0.000 description 1
- 108091005804 Peptidases Proteins 0.000 description 1
- 201000000690 abdominal obesity-metabolic syndrome Diseases 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 230000000386 athletic effect Effects 0.000 description 1
- FNAQSUUGMSOBHW-UHFFFAOYSA-H calcium citrate Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O.[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O FNAQSUUGMSOBHW-UHFFFAOYSA-H 0.000 description 1
- 239000001354 calcium citrate Substances 0.000 description 1
- 229960004256 calcium citrate Drugs 0.000 description 1
- 239000004227 calcium gluconate Substances 0.000 description 1
- 229960004494 calcium gluconate Drugs 0.000 description 1
- 235000013927 calcium gluconate Nutrition 0.000 description 1
- MKJXYGKVIBWPFZ-UHFFFAOYSA-L calcium lactate Chemical compound [Ca+2].CC(O)C([O-])=O.CC(O)C([O-])=O MKJXYGKVIBWPFZ-UHFFFAOYSA-L 0.000 description 1
- 239000001527 calcium lactate Substances 0.000 description 1
- 229960002401 calcium lactate Drugs 0.000 description 1
- 235000011086 calcium lactate Nutrition 0.000 description 1
- NEEHYRZPVYRGPP-UHFFFAOYSA-L calcium;2,3,4,5,6-pentahydroxyhexanoate Chemical compound [Ca+2].OCC(O)C(O)C(O)C(O)C([O-])=O.OCC(O)C(O)C(O)C(O)C([O-])=O NEEHYRZPVYRGPP-UHFFFAOYSA-L 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 238000005238 degreasing Methods 0.000 description 1
- 238000004925 denaturation Methods 0.000 description 1
- 230000036425 denaturation Effects 0.000 description 1
- 235000005911 diet Nutrition 0.000 description 1
- 230000037213 diet Effects 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000006911 enzymatic reaction Methods 0.000 description 1
- -1 etc. Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 235000013373 food additive Nutrition 0.000 description 1
- 239000002778 food additive Substances 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000007407 health benefit Effects 0.000 description 1
- 235000004280 healthy diet Nutrition 0.000 description 1
- 235000020256 human milk Nutrition 0.000 description 1
- 210000004251 human milk Anatomy 0.000 description 1
- 210000005075 mammary gland Anatomy 0.000 description 1
- 150000002772 monosaccharides Chemical class 0.000 description 1
- 210000003205 muscle Anatomy 0.000 description 1
- 235000020184 organic milk Nutrition 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000017854 proteolysis Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 208000001076 sarcopenia Diseases 0.000 description 1
- 230000028327 secretion Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 235000013337 tricalcium citrate Nutrition 0.000 description 1
- 208000001072 type 2 diabetes mellitus Diseases 0.000 description 1
- 235000015139 viili Nutrition 0.000 description 1
Images
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C9/00—Milk preparations; Milk powder or milk powder preparations
- A23C9/12—Fermented milk preparations; Treatment using microorganisms or enzymes
- A23C9/13—Fermented milk preparations; Treatment using microorganisms or enzymes using additives
- A23C9/1307—Milk products or derivatives; Fruit or vegetable juices; Sugars, sugar alcohols, sweeteners; Oligosaccharides; Organic acids or salts thereof or acidifying agents; Flavours, dyes or pigments; Inert or aerosol gases; Carbonation methods
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
- A23J1/00—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites
- A23J1/20—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites from milk, e.g. casein; from whey
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C9/00—Milk preparations; Milk powder or milk powder preparations
- A23C9/14—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment
- A23C9/142—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment by dialysis, reverse osmosis or ultrafiltration
- A23C9/1422—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment by dialysis, reverse osmosis or ultrafiltration by ultrafiltration, microfiltration or diafiltration of milk, e.g. for separating protein and lactose; Treatment of the UF permeate
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C9/00—Milk preparations; Milk powder or milk powder preparations
- A23C9/15—Reconstituted or recombined milk products containing neither non-milk fat nor non-milk proteins
- A23C9/1512—Reconstituted or recombined milk products containing neither non-milk fat nor non-milk proteins containing isolated milk or whey proteins, caseinates or cheese; Enrichment of milk products with milk proteins in isolated or concentrated form, e.g. ultrafiltration retentate
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P3/00—Drugs for disorders of the metabolism
- A61P3/02—Nutrients, e.g. vitamins, minerals
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C21/00—Whey; Whey preparations
- A23C21/06—Mixtures of whey with milk products or milk components
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C2210/00—Physical treatment of dairy products
- A23C2210/20—Treatment using membranes, including sterile filtration
- A23C2210/202—Treatment of milk with a membrane before or after fermentation of the milk, e.g. UF of diafiltration
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C2210/00—Physical treatment of dairy products
- A23C2210/20—Treatment using membranes, including sterile filtration
- A23C2210/206—Membrane filtration of a permeate obtained by ultrafiltration, nanofiltration or microfiltration
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C9/00—Milk preparations; Milk powder or milk powder preparations
- A23C9/14—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment
- A23C9/142—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment by dialysis, reverse osmosis or ultrafiltration
- A23C9/1427—Milk preparations; Milk powder or milk powder preparations in which the chemical composition of the milk is modified by non-chemical treatment by dialysis, reverse osmosis or ultrafiltration by dialysis, reverse osmosis or hyperfiltration, e.g. for concentrating or desalting
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
- A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
- A23L33/17—Amino acids, peptides or proteins
- A23L33/19—Dairy proteins
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Polymers & Plastics (AREA)
- Food Science & Technology (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Biochemistry (AREA)
- Water Supply & Treatment (AREA)
- Mycology (AREA)
- Proteomics, Peptides & Aminoacids (AREA)
- General Health & Medical Sciences (AREA)
- Hematology (AREA)
- Pharmacology & Pharmacy (AREA)
- Nuclear Medicine, Radiotherapy & Molecular Imaging (AREA)
- Animal Behavior & Ethology (AREA)
- Medicinal Chemistry (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Obesity (AREA)
- Organic Chemistry (AREA)
- Diabetes (AREA)
- Microbiology (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Coloring Foods And Improving Nutritive Qualities (AREA)
- Dairy Products (AREA)
- Medicines Containing Material From Animals Or Micro-Organisms (AREA)
- Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
- Peptides Or Proteins (AREA)
- Fodder In General (AREA)
Abstract
Description
本発明はホエータンパク質で強化された乳−ベース製品およびその調製方法に関する。 The present invention relates to whey protein-fortified milk-based products and methods for their preparation.
ホエータンパク質は、とりわけ運動選手の栄養摂取において、筋肉量の増加および維持における優れたタンパク質供給源であることが示されている。それゆえ、市場にはたくさんのホエータンパク質粉末およびこれを用いて製造された飲料が存在する。一般に、該ホエータンパク質製品のための原材料として、チーズ、クワルク(quark)またはカゼインホエーの限外濾過、およびそれに続く、限外濾過から得た濃縮物の乾燥によって調製される、粉末としてのホエータンパク質濃縮物が使用される。これらの製品は、チーズスターターおよびレンネットなどのスターターよって引き起こされるタンパク質分解、残留脂肪の酸化、ならびに他の風味欠陥(taste flaw)に起因して、風味が悪い(foul)という問題を有している。また、ホエー製品の製造工程の間でのミネラルの除去が、常乳の風味よりもさらに水っぽい風味を引き起こす。ホエー製品は、様々な食品添加物、矯味剤(flavoring substance)、香料製剤(flavoring preparation)および加工助剤で風味を改善することによって、風味に関連する問題を取り除くことが試みられている。 Whey protein has been shown to be an excellent source of protein in increasing and maintaining muscle mass, particularly in athletes' nutrition. Therefore, there are many whey protein powders and beverages made using them on the market. In general, whey protein as a powder, prepared by ultrafiltration of cheese, quark or casein whey, followed by drying of the concentrate obtained from ultrafiltration as the raw material for the whey protein product A concentrate is used. These products have the problem of fouling due to proteolysis caused by starters such as cheese starters and rennets, oxidation of residual fat, and other taste flaws. Yes. Also, the removal of minerals during the manufacturing process of whey products causes a more watery flavor than that of regular milk. Whey products have attempted to eliminate flavor-related problems by improving the flavor with various food additives, flavoring substances, flavoring preparations and processing aids.
現在のホエータンパク質製品の風味問題に加えて、全てのホエータンパク質が栄養価(nutrititive value)において同等でないという問題も存在する。例えば、チーズ製造の間にカゼインからホエー中へ放出されるグリコマクロペプチドの栄養価はα−ラクトアルブミンおよびβ−ラクトグロブリンの栄養価よりも小さい。グリコマクロペプチドはチーズホエーの総タンパク質のかなりの部分を構成する。 In addition to the flavor issues of current whey protein products, there is also the problem that not all whey proteins are equivalent in nutritional value. For example, the nutritional value of glycomacropeptide released from casein into whey during cheese manufacture is less than that of α-lactalbumin and β-lactoglobulin. Glycomacropeptides make up a significant portion of the total protein of cheese whey.
また、公知のホエー製品に含まれる高含有量の乳糖からさらなる問題が生じる。一般的に知られているように、乳糖は世界中で大勢の成人に対して不耐症を生じさせている。 Further problems arise from the high content of lactose contained in known whey products. As is generally known, lactose causes intolerance to many adults worldwide.
ホエータンパク質ベース製品の熱処理が、製品における構造的欠陥(structural fault)を引き起こすことも一般的に知られている。これらの製品は典型的に、薄片状(flaky)、粗い(coarse)、塊の多い(lumpy)または砂状(sandy)と表現される。 It is also generally known that heat treatment of whey protein based products causes structural defects in the product. These products are typically described as flakey, coarse, lumpy or sandy.
上記の問題に照らして、公知のホエータンパク質製品の価格−品質比率は魅力的ではない。結果、製品は一般に大規模に入手することはできないが、フィットネスセンターのような限定された施設で入手可能な専門品として消費者に提供されている。 In light of the above problems, the price-quality ratio of known whey protein products is not attractive. As a result, products are generally not available on a large scale, but are offered to consumers as specialty products available in limited facilities such as fitness centers.
乳−ベースのホエータンパク質は一般に広く知られている。乳成分を個別の画分へ分離するための様々な膜技術およびそれらの組合せもまた文献に多く記載されている。例えば、国際公開第94/13148号は、脱脂乳の精密濾過および限外濾過により非変性ホエータンパク質濃縮物を製造するための工程を開示する。カゼインは精密濾過保持液内に保持され、一方でα−ラクトアルブミンおよびβ−ラクトグロブリンは、約0.1ミクロンの細孔径を有する精密濾過膜を極めて簡単に通り抜ける。 Milk-based whey proteins are generally well known. Various membrane techniques and their combinations for separating milk components into individual fractions are also well documented in the literature. For example, WO 94/13148 discloses a process for producing a non-denatured whey protein concentrate by microfiltration and ultrafiltration of skim milk. Casein is retained in the microfiltration retentate, while α-lactalbumin and β-lactoglobulin pass very easily through microfiltration membranes having a pore size of about 0.1 microns.
国際公開第96/08155号は、精密濾過および限外濾過を利用する脱脂乳出発物質からのカゼインおよびホエータンパク質の分離を開示する。例えば、該工程によって、ホエータンパク質含有量が低下した乳飲料を製造することができる。 WO 96/08155 discloses the separation of casein and whey protein from skim milk starting material utilizing microfiltration and ultrafiltration. For example, a milk beverage having a reduced whey protein content can be produced by this process.
国際公開第00/30461号は、精密濾過が、特殊調製粉乳の調製において、アミノ酸組成を人乳に類似させるために利用され得ることを開示する。 WO 00/30461 discloses that microfiltration can be utilized to resemble the amino acid composition of human milk in the preparation of specialty formulas.
国際公開第03/094623 A1は、いくつかの膜技術、すなわち限外濾過、ナノ濾過および逆浸透が無乳糖乳飲料を調製するために利用されることを開示する。 WO 03/094623 A1 discloses that several membrane technologies, namely ultrafiltration, nanofiltration and reverse osmosis, are utilized to prepare lactose-free milk beverages.
公知の製品の欠点は有しないが、良好な風味および好ましい栄養成分を有するホエータンパク質製品を提供することが望ましい。 While not having the disadvantages of known products, it is desirable to provide a whey protein product with good flavor and favorable nutritional components.
発明の簡単な説明
我々は驚くべきことに、公知のホエータンパク質製品に関連する問題は、膜技術により調製され、α−ラクトアルブミンおよびβ−ラクトグロブリンが強化された乳−ベースホエータンパク質画分中に、カゼインを含めることによって回避できることを発見した。少量のカゼインでも、滑らかでビロードのような風味を維持するように、製品の官能特性を改善するために十分であることは驚くべきことである。驚くべきことに、本発明のホエータンパク質製品の構造および安定性もまた、いかなる砂状、薄片状、沈殿またはゲル形成等もなく良好である。また製品の栄養価も増加される。
BRIEF DESCRIPTION OF THE INVENTION We have surprisingly found that the problem associated with known whey protein products is that in a milk-based whey protein fraction prepared by membrane technology and enriched with α-lactalbumin and β-lactoglobulin. It was discovered that it can be avoided by including casein. It is surprising that a small amount of casein is sufficient to improve the sensory properties of the product so as to maintain a smooth and velvety flavor. Surprisingly, the structure and stability of the whey protein product of the present invention is also good without any sandy, flaky, precipitated or gel formed. It also increases the nutritional value of the product.
本発明の一つの実施形態において、乳のような外観および風味であるが、運動選手および他の運動に熱心な人へより有益な組成を有するホエータンパク質飲料を調製することが可能である。 In one embodiment of the present invention, it is possible to prepare a whey protein beverage that has a milky appearance and flavor but has a more beneficial composition for athletes and other exercise enthusiasts.
発明の詳細な説明
約90:10から約50:50の範囲内のカゼインに対するホエータンパク質の割合および乾量基準で少なくとも20%の総タンパク質含有量を有するホエータンパク質製品を提供することが本発明の目的である。本発明の一つの実施形態において、カゼインに対するホエータンパク質の割合は約80:20から約60:40に及ぶ。本発明の具体的な実施形態において該割合は約80:20である。
Providing a whey protein product having a total protein content of at least 20% at a rate and dry weight basis of whey protein to casein in the detailed description the range of from about 90:10 to about 50:50 invention of the present invention Is the purpose. In one embodiment of the invention, the ratio of whey protein to casein ranges from about 80:20 to about 60:40. In a specific embodiment of the invention, the ratio is about 80:20.
本発明のさらなる実施形態において、製品の総タンパク質含有量は乾量基準で30%から60%に及ぶ。本発明の具体的な実施形態において、総タンパク質量は乾量基準で40%から60%である。 In a further embodiment of the invention, the total protein content of the product ranges from 30% to 60% on a dry basis. In a specific embodiment of the invention, the total protein amount is 40% to 60% on a dry basis.
本発明のホエータンパク質製品は良好な官能特性を有し、特に、グリコマクロペプチドおよび従来型のチーズ、カードおよびカゼインホエーに存在する好ましくない代謝物によって引き起こされる異味が存在しない。加えて、本発明のホエータンパク質製品は有益な栄養学的特徴および健康上の有益な効果を有する。また、本発明のホエータンパク質製品の安定性は、薄片状、沈殿、ゲル化または構造において望ましくない変化を引き起こす他の現象は全く観察されず、良好である。 The whey protein product of the present invention has good sensory properties, especially the absence of off-flavors caused by glycomacropeptides and undesired metabolites present in conventional cheese, curd and casein whey. In addition, the whey protein product of the present invention has beneficial nutritional characteristics and health benefits. Also, the stability of the whey protein product of the present invention is good with no observable other phenomena that cause undesirable changes in flakes, precipitation, gelation or structure.
本発明の文脈において、ホエータンパク質製品とはホエータンパク質およびカゼインを含有する乳−ベースタンパク質製品を意味する。ホエータンパク質製品は、様々な膜技術およびそれらの組合せによって乳原材料から得られる一以上の様々な成分から調製することができる。ホエータンパク質製品はさらに乳由来のミネラルを含むことができる。乳原材料は乳そのもの、または濃縮物もしくは所望の方法により前処理された乳であってもよい。乳原材料は、脂肪、タンパク質または糖類画分などの乳製品の調製において一般的に使用される原料で補充されてもよい。乳原材料はそれゆえ、例えば、全脂肪乳、クリーム、低脂肪乳もしくは脱脂乳、限外濾過乳、透析濾過乳、精密濾過乳、無乳糖乳もしくは低乳糖乳、タンパク質分解酵素処理乳、粉乳からの還元乳、有機乳、あるいはこれらの組合せ、またはこれらのいずれかの希釈物であってもよい。乳はウシ、ヒツジ、ヤギ、ラクダ、ウマまたは栄養に適している乳を産生する任意の他の動物に由来することができる。乳は好ましくは低脂肪乳または脱脂乳である。本発明のさらに好ましい実施形態において、ホエータンパク質製品は脱脂乳から調製される。 In the context of the present invention, whey protein product means a milk-based protein product containing whey protein and casein. Whey protein products can be prepared from one or more different ingredients obtained from dairy ingredients by various membrane techniques and combinations thereof. The whey protein product can further include milk-derived minerals. The dairy ingredient may be milk itself, or a concentrate or milk that has been pretreated by a desired method. The dairy ingredients may be supplemented with ingredients commonly used in the preparation of dairy products such as fat, protein or sugar fractions. Milk raw materials are therefore derived from, for example, full-fat milk, cream, low-fat or skim milk, ultrafiltered milk, diafiltered milk, microfiltered milk, lactose-free or low-lactose milk, proteolytic enzyme-treated milk, powdered milk Reduced milk, organic milk, or combinations thereof, or dilutions of any of these. The milk can be derived from cows, sheep, goats, camels, horses or any other animal that produces milk suitable for nutrition. The milk is preferably low fat milk or skim milk. In a further preferred embodiment of the invention, the whey protein product is prepared from skim milk.
本発明のホエータンパク質製品は、飲料のような液体、濃縮物または粉末として提供され得る。本発明の具体的な実施形態において、ホエータンパク質製品は飲料である。飲料は、飲料の重量に基づいて典型的には2.5重量%から8重量%の、好ましくは3.5重量%から6重量%の総タンパク質含有量を有する。カゼインは総タンパク質含有量の5%から50%、好ましくは15%から25%を構成し、一方、α−ラクトアルブミンとβ−ラクトグロブリンで強化されたホエータンパク質は50%から95%、好ましくは75%から85%を構成する。 The whey protein product of the present invention may be provided as a beverage-like liquid, concentrate or powder. In a specific embodiment of the invention, the whey protein product is a beverage. Beverages typically have a total protein content of 2.5% to 8% by weight, preferably 3.5% to 6% by weight, based on the weight of the beverage. Casein constitutes 5% to 50%, preferably 15% to 25% of the total protein content, while whey protein enriched with α-lactalbumin and β-lactoglobulin is 50% to 95%, preferably It constitutes 75% to 85%.
糖類、甘味料または香味料を含有しないことは本発明のホエータンパク質製品の特徴であるが、しかしながらこの実施形態へ限定されるものではない。本発明の具体的な実施形態において、ホエータンパク質製品はインスタント用に準備された(ready for instant use)飲料であり、飲料内に糖類、甘味料または香味料は一切含有されない。 The absence of sugars, sweeteners or flavors is a feature of the whey protein product of the present invention, however, it is not limited to this embodiment. In a specific embodiment of the invention, the whey protein product is a ready for instant use beverage and does not contain any sugars, sweeteners or flavors in the beverage.
牛乳のミネラル組成のように、本発明のホエータンパク質製品のミネラル組成は非常に生理的である。例えば、本発明のホエータンパク質飲料は典型的に0.5%から1.5%の、好ましくは0.6%から0.8%のミネラルを含有することができる。しかしながら本発明のホエータンパク質製品のカルシウム含有量は常乳のそれよりも低い。ホエータンパク質製品はそれゆえ、補助的カルシウムおよび他の乳ミネラル類、例えば、以下に記載する本発明の工程から得られるナノ濾過透過液を付与され得る。補助的カルシウムはそれゆえ、乳カルシウム、グルコン酸カルシウム、クエン酸カルシウム、乳酸カルシウムなど、またはそれらの混合物のような、任意のカルシウム供給源として提供され得る。 Like the mineral composition of milk, the mineral composition of the whey protein product of the present invention is very physiological. For example, the whey protein beverage of the present invention can typically contain 0.5% to 1.5% minerals, preferably 0.6% to 0.8%. However, the calcium content of the whey protein product of the present invention is lower than that of regular milk. The whey protein product can therefore be supplemented with supplemental calcium and other milk minerals such as the nanofiltration permeate resulting from the inventive process described below. Supplemental calcium can therefore be provided as any calcium source, such as milk calcium, calcium gluconate, calcium citrate, calcium lactate, etc., or mixtures thereof.
脂肪もまた本発明のホエータンパク質製品中に含有され得る。製品の脂肪含有量は典型的に約0%から最高で3.5%まで及ぶ。 Fats can also be included in the whey protein product of the present invention. The fat content of the product typically ranges from about 0% up to 3.5%.
本発明の一つの実施形態において、ホエータンパク質製品は低乳糖または無乳糖である。低乳糖または無乳糖製品は、製品の調製のために使用される膜技術によって得ることができる。また、ホエータンパク質製品中のいかなる残存乳糖も、酵素法によって加水分解され得る。本発明の文脈において、「低乳糖」とはホエータンパク質製品において1%未満の乳糖含有量を意味する。「無乳糖」とはホエータンパク質製品の乳糖含有量が、一食あたり0.5gである(例えば、液体乳について0.5g/244g、乳糖含有量は最大でも0.21%である)が、しかしながら0.5%を超えないことを意味する。本発明に従って、炭水化物をほとんど含有せず、完璧な官能特性を有するホエータンパク質飲料もまた製造できる。 In one embodiment of the invention, the whey protein product is low or no lactose. Low lactose or lactose-free products can be obtained by the membrane technology used for the preparation of the product. Any residual lactose in the whey protein product can also be hydrolyzed by enzymatic methods. In the context of the present invention, “low lactose” means a lactose content of less than 1% in the whey protein product. “Lactose-free” means that the whey protein product has a lactose content of 0.5 g per serving (eg, 0.5 g / 244 g for liquid milk, with a lactose content of at most 0.21%). It means not exceeding 0.5%. In accordance with the present invention, whey protein beverages that contain little carbohydrate and have perfect sensory characteristics can also be produced.
本発明のホエータンパク質製品は、全ての種類の酸乳製品および/または酸性化生鮮製品(acidified fresh product)、典型的には、ヨーグルト、発酵乳、ヴィーリ(viili)、発酵クリーム、サワークリーム、クワルク(quark)、バターミルク、ケフィア、小容量の乳飲料(dairy shot drink)、および他の酸乳製品の調製における原材料として使用することができる。我々は驚くべきことに、本発明のホエータンパク質製品から調製された酸乳製品の官能特性が従来の酸乳製品の官能特性に類似していることを発見した。 The whey protein products of the present invention are all kinds of sour milk products and / or acidified fresh products, typically yogurt, fermented milk, viili, fermented cream, sour cream, quark ( quark), buttermilk, kefir, small volume milk drinks, and other sour dairy products can be used as a raw material. We have surprisingly found that the sensory characteristics of sour milk products prepared from the whey protein product of the present invention are similar to those of conventional sour milk products.
本発明の製品は、食品、動物飼料、栄養製品、栄養補助食品、食品原料、健康食品および医薬品からなる群から選択することができるが、これらに限定されない。本発明の一つの実施形態において、製品は食品または飼料製品である。本発明の別の実施形態において、製品は機能性食品、すなわち健康を促進する、かつ/または疾患を予防および/または軽減する何らかの特性を有する食品である。食品、食品材料および/または医薬品、および動物飼料の各々の形式は特に限定されない。 The product of the present invention can be selected from the group consisting of food, animal feed, nutritional products, nutritional supplements, food ingredients, health foods and pharmaceuticals, but is not limited thereto. In one embodiment of the invention, the product is a food or feed product. In another embodiment of the invention, the product is a functional food, i.e. a food having some property that promotes health and / or prevents and / or reduces disease. Each form of food, food material and / or pharmaceutical, and animal feed is not particularly limited.
上述の通り、その有益な栄養成分に起因して、本発明のホエータンパク質製品は、そのものまたは日常の食事の一部として運動選手および他の運動に熱心な人に対して好適である。本発明は、健康的な食事を支持するまたは改善するためのホエータンパク質を含む組成物を提供する。製品はまた、特に成人発症の糖尿病、代謝症候群およびサルコペニアの緩和および/または予防に関連して有益である。 As mentioned above, due to its beneficial nutritional components, the whey protein product of the present invention is suitable for athletes and other athletic people as such or as part of their daily diet. The present invention provides a composition comprising whey protein for supporting or improving a healthy diet. The product is also beneficial particularly in connection with the alleviation and / or prevention of adult-onset diabetes, metabolic syndrome and sarcopenia.
本発明の別の目的は、食品、動物飼料、栄養製品、栄養補助食品、食品原料、健康食品および医薬品としてのホエータンパク質製品の使用を提供することである。本発明の一つの実施形態において、製品は機能性食品および/または栄養製品として提供される。別の実施態様において、製品は医薬品として提供される。 Another object of the present invention is to provide the use of whey protein products as food, animal feed, nutritional products, nutritional supplements, food ingredients, health foods and pharmaceuticals. In one embodiment of the invention, the product is provided as a functional food and / or nutritional product. In another embodiment, the product is provided as a medicament.
ホエータンパク質製品は、膜技術によって得られた一以上の画分から製造される。適切な方法で、精密濾過、限外濾過、ナノ濾過および逆浸透を含む二以上の技術を組み合わせることができる。本発明のさらなる目的はそれゆえ、
−精密濾過透過液としての理想的なホエーおよび精密濾過保持液としてのカゼイン濃縮物を分離するために、乳−ベース原材料を精密濾過に供すること、
−限外濾過透過液および限外濾過保持液としてのホエータンパク質濃縮物を提供するために、精密濾過透過液の少なくとも一部分を限外濾過に供すること、
−約90:10から約50:50の範囲内のカゼインに対するホエータンパク質の割合および乾量基準で少なくとも20%の総タンパク質含有量を提供するように、限外濾過保持液およびカゼイン含有物質、および、所望により、他の原料から、ホエータンパク質製品を構成すること、
を含む、ホエータンパク質製品を製造するための方法を提供することである。
Whey protein products are produced from one or more fractions obtained by membrane technology. In an appropriate manner, two or more techniques can be combined including microfiltration, ultrafiltration, nanofiltration and reverse osmosis. A further object of the present invention is therefore
-Subjecting the milk-base raw material to microfiltration to separate ideal whey as microfiltration permeate and casein concentrate as microfiltration retentate;
-Subjecting at least a portion of the microfiltration permeate to ultrafiltration to provide an ultrafiltration permeate and a whey protein concentrate as ultrafiltration retentate;
A ratio of whey protein to casein in the range of about 90:10 to about 50:50 and a total protein content of at least 20% on a dry basis, and ultrafiltration retentate and casein-containing material, and Configuring whey protein products from other ingredients, if desired,
To provide a method for producing a whey protein product.
乳−ベース原材料は好ましくは脱脂乳である。 The milk-based raw material is preferably skim milk.
本発明の一つの実施形態において、カゼイン含有物質は本発明の方法において得られる精密濾過保持液である。別の実施形態において、カゼイン含有物質は乳である。本明細書において用いる場合、用語「乳」は、ウシの、ヒツジの、ヤギの、ラクダの、ウマの、または栄養に適している乳を産生する任意の他の動物などの、ほ乳動物の乳腺から得られる任意の正常分泌物を意味する。乳は、脂肪、タンパク質または糖類画分などの乳製品の調製において一般的に使用される原料で補充できる。乳はそれゆえ、例えば、全脂肪乳、低脂肪乳もしくは脱脂乳、クリーム、限外濾過乳(UF保持液)、透析濾過乳、精密濾過乳(MF透過液)、粉乳からの還元乳、有機乳、あるいはこれらの組合せ、またはこれらのいずれかの希釈物を含む。 In one embodiment of the invention, the casein-containing substance is a microfiltration retentate obtained in the method of the invention. In another embodiment, the casein-containing material is milk. As used herein, the term “milk” refers to the mammary gland of a mammal, such as bovine, sheep, goat, camel, horse, or any other animal that produces nutritionally suitable milk. Means any normal secretion obtained from Milk can be supplemented with ingredients commonly used in the preparation of dairy products such as fat, protein or sugar fractions. Milk is therefore, for example, full fat milk, low fat milk or skim milk, cream, ultrafiltered milk (UF retentate), diafiltered milk, microfiltered milk (MF permeate), reduced milk from powdered milk, organic Contains milk, or combinations thereof, or dilutions of any of these.
本発明の一つの実施形態において、乳は脱脂乳である。本発明の別の実施形態において、乳は低乳糖乳もしくは無乳糖乳である。 In one embodiment of the invention, the milk is skim milk. In another embodiment of the invention, the milk is low or non-lactose milk.
ホエータンパク質製品を構成した後、適切な場合には、自体公知の方法により熱処理することができる。 After constructing the whey protein product, if appropriate, it can be heat treated by methods known per se.
本発明の1つの実施形態において、ミネラル、および乳糖を含む糖類の大部分を含有する限外濾過透過液の少なくとも一部分は、ミネラルをNF透過液中へ、および糖類をNF保持液中へ分離するために、さらにナノ濾過(NF)へ供することができる。別の実施形態において、NF透過液の少なくとも一部分は、RO保持液中へミネラルを濃縮するために、またさらに逆浸透(RO)へ供することができる。上記のさらなる膜濾過から得られたこれらの画分は、本発明のホエータンパク質製品を構成するために利用することができる。本発明の一つの実施形態において、精密濾過保持液、限外濾過保持液およびナノ濾過透過液は、本発明のホエータンパク質製品の調製において使用される。本発明の別の実施形態において、精密濾過保持液、限外濾過保持液および逆浸透保持液は、本発明のホエータンパク質製品の調製において使用される。 In one embodiment of the invention, at least a portion of the ultrafiltration permeate containing a majority of the sugars including minerals and lactose separates the minerals into the NF permeate and the sugars into the NF retentate. Therefore, it can be further subjected to nanofiltration (NF). In another embodiment, at least a portion of the NF permeate can be subjected to reverse osmosis (RO) to concentrate the mineral into the RO retentate and further. These fractions obtained from the above further membrane filtration can be utilized to construct the whey protein product of the present invention. In one embodiment of the invention, microfiltration retentate, ultrafiltration retentate and nanofiltration permeate are used in the preparation of the whey protein product of the invention. In another embodiment of the invention, microfiltration retentate, ultrafiltration retentate and reverse osmosis retentate are used in the preparation of the whey protein product of the invention.
本発明のさらなる実施形態において、精密濾過(MF)、限外濾過(UF)および/またはナノ濾過(NF)は、水または膜濾過から得られた好適な画分を使用する透析濾過によって増強される。透析濾過が精密濾過に付随する時、MF透過液の限外濾過から得られるUF透過液はダイアウォーター(diawater)として適切に使用される。UF透過液がさらにナノ濾過へ供される時、NF透過液は限外濾過におけるダイアウォーターとして適切に使用される。NF透過液がまたさらに逆浸透(RO)へ供される時、RO透過液はナノ濾過におけるダイアウォーターとして適切に使用される。該透析濾過段階の一以上を本発明の工程において使用することができる。 In a further embodiment of the invention, microfiltration (MF), ultrafiltration (UF) and / or nanofiltration (NF) is enhanced by diafiltration using suitable fractions obtained from water or membrane filtration. The When diafiltration is associated with microfiltration, the UF permeate obtained from ultrafiltration of the MF permeate is suitably used as a diawater. When the UF permeate is further subjected to nanofiltration, the NF permeate is suitably used as diawater in ultrafiltration. When the NF permeate is also subjected to further reverse osmosis (RO), the RO permeate is suitably used as diawater in nanofiltration. One or more of the diafiltration steps can be used in the process of the present invention.
本発明の方法は、風味および食感などの良好な官能特性を有し、良好な安定性を備えるホエータンパク質製品を提供する。該方法によって、ホエータンパク質製品に対して好ましくない異味を引き起こすグリコマクロペプチドおよび代謝物の放出を抑えることができる。それゆえ、本発明の方法を実行することにより、ホエータンパク質製品の異味を減少し、除去し、または隠すことができる。 The method of the present invention provides a whey protein product with good sensory characteristics such as flavor and texture and with good stability. The method can suppress the release of glycomacropeptides and metabolites that cause objectionable tastes to whey protein products. Therefore, by implementing the method of the present invention, the off-taste of the whey protein product can be reduced, eliminated or masked.
従来の研究からホエータンパク質の栄養価において違いが存在することが示されている。より具体的には、α−ラクトアルブミンがβ−ラクトグロブリンよりもより有益な栄養価を有しているということが発見されている。この知見に基づき、本発明のホエータンパク質製品の組成は適切な方法により様々な用途へと調整できる。本発明において、ホエータンパク質組成の調整は、乳原材料の熱処理によって、または膜の選択によって達成される。本発明の工程は、乳製品の熱処理における自体公知の技術を使用する。本発明の工程において使用される熱処理の例は、低温殺菌、高温殺菌あるいは低温殺菌温度より低い温度での十分長い時間の加熱である。特に、UHT処理(例えば乳の場合、138℃で2−4秒)、ESL処理(例えば乳の場合、130℃で1−2秒)、低温殺菌(例えば乳の場合、72℃で15秒)、または高温殺菌(例えば乳の場合、95℃で5分)を挙げることができる。熱処理は、直接的(蒸気を乳へ、乳を蒸気へ)または間接的(チューブ式熱交換器、プレート式熱交換器、表面かき取り式熱交換器)のいずれであってもよい。 Previous studies have shown that differences exist in the nutritional value of whey protein. More specifically, it has been discovered that α-lactalbumin has a more beneficial nutritional value than β-lactoglobulin. Based on this knowledge, the composition of the whey protein product of the present invention can be adjusted to various uses by an appropriate method. In the present invention, the adjustment of the whey protein composition is achieved by heat treatment of the dairy ingredients or by membrane selection. The process of the invention uses techniques known per se in the heat treatment of dairy products. Examples of heat treatments used in the process of the present invention are pasteurization, pasteurization or heating for a sufficiently long time at a temperature below the pasteurization temperature. In particular, UHT treatment (for example for milk, 138 ° C. for 2-4 seconds), ESL treatment (for example for milk, 130 ° C. for 1-2 seconds), pasteurization (for example, for milk, 72 ° C. for 15 seconds) Or high temperature sterilization (for example, at 95 ° C. for 5 minutes in the case of milk). The heat treatment may be either direct (steam to milk, milk to steam) or indirectly (tube heat exchanger, plate heat exchanger, scraped surface heat exchanger).
本発明の1つの実施形態において、ホエータンパク質原料を選択的に分離するために、乳は精密濾過に先立って、65℃から95℃の温度範囲で15秒間から10分間の熱処理に供される。熱処理の結果として、β−ラクトグロブリンは変性されカゼインに結合する一方、α−ラクトアルブミンは膜を通過する。この方法で、α−ラクトアルブミンの含有量を精密濾過透過液において増加させることができる。 In one embodiment of the invention, the milk is subjected to a heat treatment for 15 seconds to 10 minutes at a temperature range of 65 ° C. to 95 ° C. prior to microfiltration to selectively separate the whey protein material. As a result of the heat treatment, β-lactoglobulin is denatured and binds to casein, while α-lactalbumin passes through the membrane. In this way, the content of α-lactalbumin can be increased in the microfiltration permeate.
本発明の1つの実施形態において、乳原材料における本発明のホエータンパク質製品における乳糖は、その分野において周知であるように、単糖類へと加水分解される。これは自体公知の方法において市販の乳糖分解酵素で行うことができる。本発明の1つの実施形態において、乳糖加水分解は構成されたホエータンパク質製品の膜濾過の後に実行される。本発明の別の実施形態において、乳糖加水分解段階および精密濾過段階は、互いに同時に開始される。本発明のさらに別の実施形態において、乳原材料の乳糖加水分解は膜濾過段階に先立って開始される。 In one embodiment of the invention, the lactose in the whey protein product of the invention in the dairy material is hydrolyzed to monosaccharides as is well known in the art. This can be done with commercially available lactose degrading enzymes in a manner known per se. In one embodiment of the invention, lactose hydrolysis is performed after membrane filtration of the configured whey protein product. In another embodiment of the invention, the lactose hydrolysis stage and the microfiltration stage are initiated simultaneously with each other. In yet another embodiment of the invention, lactose hydrolysis of the dairy material is initiated prior to the membrane filtration step.
乳糖加水分解は、例えば、本発明の方法において得られた様々な画分(UF保持液およびMF保持液)の後期に構成されたホエータンパク質製品の熱処理によって、乳糖分解酵素が不活化するまで継続することができる。 Lactose hydrolysis continues, for example, until the lactose-degrading enzyme is inactivated by heat treatment of the whey protein product constructed in the later stages of the various fractions obtained in the method of the present invention (UF retentate and MF retentate) can do.
以下の実施例は本発明のさらなる説明を示すが、本発明を限定するものではない。 The following examples illustrate further the invention but do not limit the invention.
脱脂乳(1000L)を800kDaの細孔径を有する高分子濾過膜(Synder FR)によって精密濾過する。透析濾過段階を含み、濃縮係数95が使用される。濃縮係数は式1によって計算される。形成された精密濾過保持液の量は20.0%の乾物含量を有する190Lである。
(式1)
Skim milk (1000 L) is microfiltered through a polymer filtration membrane (Synder FR) having a pore size of 800 kDa. A diafiltration step is included, and a concentration factor of 95 is used. The concentration factor is calculated by Equation 1. The amount of microfiltration retentate formed is 190 L with a dry matter content of 20.0%.
(Formula 1)
精密濾過において形成される透過液(1890L)はさらに10kDaの細孔径を有する高分子限外濾過(UF)膜(Koch HFK−131)によって濾過される。限外濾過から得られた透過液はさらにナノ濾過(NF)へ供され、NF保持液および透過液(130L)を得る。 The permeate (1890L) formed in the microfiltration is further filtered through a polymer ultrafiltration (UF) membrane (Koch HFK-131) having a pore size of 10 kDa. The permeate obtained from the ultrafiltration is further subjected to nanofiltration (NF) to obtain an NF retentate and permeate (130 L).
限外濾過は、ダイアウォーターとして上述の130LのNF透過液を使用する透析濾過によって実行される。限外濾過の総濃縮係数は24である(式1)。限外濾過において、100Lの限外濾過保持液、および1920Lの限外濾過透過液が形成され、その1080Lが精密濾過の透析濾過のために使用される。残りの限外濾過透過液(840L)は200Daのカットオフ値を有する濾過膜(Desal 5−DK)によってナノ濾過される。ナノ濾過の濃縮係数は4.25であり(式1)、197Lのナノ濾過保持液および644Lのナノ濾過透過液が形成され、後者の130Lは、上述の通り、精密濾過透過液の限外濾過の透析濾過におけるダイアウォーターとして使用される。 Ultrafiltration is performed by diafiltration using the 130 L NF permeate described above as diawater. The total concentration factor for ultrafiltration is 24 (Equation 1). In the ultrafiltration, 100 L of ultrafiltration retentate and 1920 L of ultrafiltration permeate are formed and 1080 L is used for diafiltration for microfiltration. The remaining ultrafiltration permeate (840L) is nanofiltered through a filtration membrane (Desal 5-DK) with a cutoff value of 200 Da. The concentration factor of nanofiltration is 4.25 (Equation 1), 197 L of nanofiltration retentate and 644 L of nanofiltration permeate are formed, the latter 130 L is ultrafiltration of microfiltration permeate as described above It is used as diawater in diafiltration.
精密濾過透過液の限外濾過の透析濾過におけるダイアウォーターとしては使用されない残存ナノ濾過透過液は、他の目的のために使用され、あるいは、濃縮係数10(式1)の使用により逆浸透膜(Koch HR)によって濃縮される。形成されたナノ濾過透過液の逆浸透透過液の量は500Lであり、その44Lがナノ濾過の透析濾過におけるダイアウォーターとして使用される。形成されたナノ濾過透過液の逆浸透保持液の量は55Lである。 The remaining nanofiltration permeate not used as diawater in the diafiltration of ultrafiltration permeation of the microfiltration permeate can be used for other purposes or by using a reverse osmosis membrane (by using a concentration factor of 10 (Equation 1)) Koch HR). The amount of reverse osmosis permeate in the nanofiltration permeate formed is 500 L, and 44 L is used as diawater in diafiltration of nanofiltration. The amount of the reverse osmosis retentate of the formed nanofiltration permeate is 55L.
脱脂乳(1000L)は、熱処理装置において65℃から95℃の温度範囲で15秒間から10分間の熱処理に供され、ホエータンパク質原料を選択的に分離する。β−ラクトグロブリンが1−90%の程度で変性される一方、0−26%の変性度を有し熱不安定性のより低いα−ラクトアルブミンで精密濾過透過液が強化されるように、脱脂乳の熱処理は精密濾過におけるホエータンパク質の透過に影響する。脱脂乳の熱処理の後、乳は実施例1に記載されるように濾過手順へ供される。 The skim milk (1000 L) is subjected to a heat treatment for 15 seconds to 10 minutes in a temperature range of 65 ° C. to 95 ° C. in a heat treatment apparatus to selectively separate the whey protein raw material. Degreasing so that β-lactoglobulin is denatured to the extent of 1-90% while microfiltration permeate is enhanced with α-lactalbumin having a degree of denaturation of 0-26% and less thermal instability. Milk heat treatment affects the permeation of whey protein in microfiltration. After heat treatment of skim milk, the milk is subjected to a filtration procedure as described in Example 1.
一例として、精密濾過透過液中のα−ラクトアルブミンおよびβ−ラクトグロブリンの総量のうちα−ラクトアルブミンの割合(重量%)は38%(30秒間75℃の熱処理)から45%(30秒間90℃の熱処理)であった。 As an example, the proportion (% by weight) of α-lactalbumin in the total amount of α-lactalbumin and β-lactoglobulin in the microfiltration permeate is from 38% (heat treatment at 75 ° C. for 30 seconds) to 45% (90 seconds for 30 seconds). Heat treatment).
本発明によるホエータンパク質製品は、表1に示されるように、実施例1の精密濾過保持液および限外濾過保持液から構成された。製品の、ホエータンパク質のカゼインに対する割合は80:20であり、タンパク質含有量は乾量基準で58%であった。製品は、乳糖が、構成後に酵素的に加水分解された、低乳糖乳飲料であった。 The whey protein product according to the present invention was composed of the microfiltration retentate and ultrafiltration retentate of Example 1 as shown in Table 1. The ratio of product to whey protein casein was 80:20 and the protein content was 58% on a dry basis. The product was a low lactose milk beverage in which lactose was enzymatically hydrolyzed after composition.
教育を受けた熟練のパネルが製品を官能的に評価した。官能特性は「非常に良好」であった。食感に影響する風味欠陥および構造的欠陥は全く観察されなかった。
本発明によるホエータンパク質製品は、表2に示されるように、実施例1の精密濾過保持液、限外濾過保持液およびナノ濾過保持液、および水から構成された。製品の、ホエータンパク質のカゼインに対する割合は80:20であり、タンパク質含有量は乾量基準で43%であった。 As shown in Table 2, the whey protein product according to the present invention was composed of the microfiltration retentate of Example 1, the ultrafiltration retentate and the nanofiltration retentate, and water. The ratio of product to whey protein casein was 80:20, and the protein content was 43% on a dry basis.
教育を受けた熟練のパネルが製品を官能的に評価した。官能特性は「非常に良好」であった。食感に影響する風味欠陥および構造的欠陥は全く観察されなかった。
本発明によるホエータンパク質製品は、表3に示されるように、実施例1の精密濾過保持液、限外濾過保持液、ナノ濾過保持液およびナノ濾過透過液から構成された。製品の、ホエータンパク質のカゼインに対する割合は60:40であり、タンパク質含有量は乾量基準で38%であった。 The whey protein product according to the present invention was composed of the microfiltration retentate, ultrafiltration retentate, nanofiltration retentate and nanofiltration permeate of Example 1 as shown in Table 3. The ratio of product to whey protein casein was 60:40, and the protein content was 38% on a dry basis.
教育を受けた熟練のパネルが製品を官能的に評価した。官能特性は「非常に良好」であった。食感に影響する風味欠陥および構造的欠陥は全く観察されなかった。
本発明によるホエータンパク質製品は、表4に示されるように、実施例1の精密濾過保持液、限外濾過保持液およびナノ濾過保持液、乳ミネラル粉末および水から構成された。ホエータンパク質のカゼインに対する割合は50:50であり、タンパク質含有量は乾量基準で48%であった。製品は、乳糖が、構成後に0.1%未満のレベルへ酵素的に加水分解された、無乳糖乳飲料であった。 As shown in Table 4, the whey protein product according to the present invention was composed of the microfiltration retentate, ultrafiltration retentate and nanofiltration retentate of Example 1, milk mineral powder and water. The ratio of whey protein to casein was 50:50, and the protein content was 48% on a dry basis. The product was a lactose-free milk drink in which lactose was hydrolyzed enzymatically to a level of less than 0.1% after composition.
教育を受けた熟練のパネルが製品を官能的に評価した。官能特性は「非常に良好」であった。食感に影響する風味欠陥および構造的欠陥は全く観察されなかった。
本発明によるホエータンパク質製品は、表5に示されるように、実施例1の精密濾過保持液、限外濾過保持液、ナノ濾過保持液および逆浸透保持液、および水から構成された。製品のホエータンパク質のカゼインに対する割合は70:30であり、そのタンパク質含有量は乾量基準で51%であった。製品は、乳糖が、構成後に0.1%未満のレベルへ酵素的に加水分解された、無乳糖乳飲料であった。 The whey protein product according to the present invention was composed of the microfiltration retentate, ultrafiltration retentate, nanofiltration retentate and reverse osmosis retentate, and water of Example 1, as shown in Table 5. The ratio of product whey protein to casein was 70:30 and its protein content was 51% on a dry basis. The product was a lactose-free milk drink in which lactose was hydrolyzed enzymatically to a level of less than 0.1% after composition.
教育を受けた熟練のパネルが製品を官能的に評価した。官能特性は「非常に良好」であった。食感に影響する風味欠陥および構造的欠陥は全く観察されなかった。
本発明によるホエータンパク質製品は、表6に示されるように、乳および実施例1の限外濾過保持液から構成された。製品のホエータンパク質のカゼインに対する割合は70:30であり、タンパク質含有量は乾量基準で48%であった。 The whey protein product according to the present invention was composed of milk and the ultrafiltration retentate of Example 1 as shown in Table 6. The ratio of product whey protein to casein was 70:30 and protein content was 48% on a dry basis.
教育を受けた熟練のパネルが製品を官能的に評価した。官能特性は「非常に良好」であった。食感に影響する風味欠陥および構造的欠陥は全く観察されなかった。
Claims (34)
−精密濾過透過液としての理想的なホエー、および精密濾過保持液としてのカゼイン濃縮物を分離するために、乳−ベース原材料を精密濾過に供すること、
−限外濾過透過液および限外濾過保持液としてのホエータンパク質濃縮物を提供するために、精密濾過透過液の少なくとも一部分を限外濾過に供すること、
−90:10から50:50の範囲内のカゼインに対するホエータンパク質の割合および乾量基準で少なくとも20%の総タンパク質含有量を提供するように、限外濾過保持液およびカゼイン含有物質を含むホエータンパク質製品を提供すること、
を含む、方法。 A method for producing a whey protein product comprising:
Subjecting the milk-based raw material to microfiltration to separate the ideal whey as microfiltration permeate and casein concentrate as microfiltration retentate;
-Subjecting at least a portion of the microfiltration permeate to ultrafiltration to provide an ultrafiltration permeate and a whey protein concentrate as ultrafiltration retentate;
Whey protein comprising ultrafiltration retentate and casein-containing material to provide a ratio of whey protein to casein in the range of 90:10 to 50:50 and a total protein content of at least 20% on a dry basis Providing products,
Including a method.
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI20096114 | 2009-10-28 | ||
US12/607,367 US20110097442A1 (en) | 2009-10-28 | 2009-10-28 | Whey protein product and a method for its preparation |
FI20096114A FI122675B (en) | 2009-10-28 | 2009-10-28 | Whey protein product and a method for its preparation |
US12/607,367 | 2009-10-28 |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2012535891A Division JP2013509171A (en) | 2009-10-28 | 2010-10-25 | Whey protein product and preparation method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2015221041A true JP2015221041A (en) | 2015-12-10 |
JP6509058B2 JP6509058B2 (en) | 2019-05-08 |
Family
ID=43530234
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2012535891A Pending JP2013509171A (en) | 2009-10-28 | 2010-10-25 | Whey protein product and preparation method thereof |
JP2015132362A Active JP6509058B2 (en) | 2009-10-28 | 2015-07-01 | Whey protein product and method for preparing the same |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2012535891A Pending JP2013509171A (en) | 2009-10-28 | 2010-10-25 | Whey protein product and preparation method thereof |
Country Status (15)
Country | Link |
---|---|
EP (1) | EP2493325B1 (en) |
JP (2) | JP2013509171A (en) |
KR (1) | KR20120098753A (en) |
CN (2) | CN102595915A (en) |
AR (1) | AR078779A1 (en) |
AU (1) | AU2010311316B2 (en) |
BR (1) | BR112012009744B1 (en) |
CA (1) | CA2778360A1 (en) |
DK (1) | DK2493325T3 (en) |
ES (1) | ES2852749T3 (en) |
IL (1) | IL219403A (en) |
LT (1) | LT2493325T (en) |
MX (1) | MX2012004738A (en) |
PL (1) | PL2493325T3 (en) |
WO (1) | WO2011051557A1 (en) |
Families Citing this family (35)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
MX2012004738A (en) | 2009-10-28 | 2012-05-23 | Valio Ltd | Whey protein product and a method for its preparation. |
FI124323B (en) | 2011-02-18 | 2014-06-30 | Valio Oy | Milk-based product and process for its preparation |
FI124711B (en) * | 2011-07-06 | 2014-12-15 | Valio Oy | Milk-based formulation |
FI124816B (en) * | 2011-08-31 | 2015-02-13 | Valio Oy | Process for the preparation of a product containing physically modified fat globules and a product made by the process |
FI125332B (en) * | 2011-11-11 | 2015-08-31 | Valio Oy | Process for the preparation of a milk product |
WO2013137714A1 (en) | 2012-03-12 | 2013-09-19 | N.V. Nutricia | Process for the humanization of animal skim milk and products obtained thereby |
CN102630803A (en) * | 2012-05-15 | 2012-08-15 | 东北农业大学 | Humanized milk protein and preparation method thereof |
FI126558B (en) | 2012-06-27 | 2017-02-15 | Valio Oy | New casein protein product and process for its preparation |
DK2730170T3 (en) * | 2012-11-13 | 2016-05-30 | Dmk Deutsches Milchkontor Gmbh | Allergen-free food compositions |
WO2014163486A1 (en) | 2013-04-03 | 2014-10-09 | N.V. Nutricia | Process and system for preparing dry milk formulae |
WO2014163485A1 (en) * | 2013-04-03 | 2014-10-09 | N.V. Nutricia | Process and system for preparing dry milk formulae |
JP6330263B2 (en) * | 2013-06-06 | 2018-05-30 | 日本新薬株式会社 | Acidic liquid food composition |
CN103349077B (en) * | 2013-07-01 | 2015-05-20 | 南昌大学 | Preparation method of high anti-oxidant milk powder addictive |
WO2015041515A1 (en) * | 2013-09-19 | 2015-03-26 | N.V. Nutricia | Improved process for the humanization of animal skim milk |
ES2667705T3 (en) | 2013-11-15 | 2018-05-14 | Grenade (Uk) Ltd | Food compositions |
CN106455653A (en) * | 2014-03-26 | 2017-02-22 | 雅培公司 | Nutritional supplement powder |
CN103876146A (en) * | 2014-04-01 | 2014-06-25 | 吉林大学 | Rana japonica oil polypeptide lozenges and preparation method thereof |
FI129057B (en) * | 2014-12-22 | 2021-06-15 | Valio Oy | A method for producing a spoonable acidified milk product |
FI126179B (en) | 2015-02-12 | 2016-07-29 | Valio Oy | Process for producing a milk-based product |
FI129567B (en) * | 2015-08-31 | 2022-04-29 | Valio Oy | Method for producing a milk-based product |
CN105348379A (en) * | 2015-12-16 | 2016-02-24 | 新希望双喜乳业(苏州)有限公司 | Method for extracting beta-lactoglobulin from milk |
CN105341316A (en) * | 2015-12-16 | 2016-02-24 | 新希望双喜乳业(苏州)有限公司 | Method for extracting high-purity whey protein from milk |
WO2017142494A1 (en) * | 2016-02-15 | 2017-08-24 | Gebze Teknik Universitesi | A method for high volume recovery of process- water and economic product acquisition from whey |
WO2017194068A1 (en) * | 2016-05-12 | 2017-11-16 | Arla Foods Amba | Whey preparation for improving brain development |
IL310614A (en) * | 2016-07-06 | 2024-04-01 | Building Block Nutritionals Llc | Nutritional formula |
WO2018028765A1 (en) * | 2016-08-08 | 2018-02-15 | Compagnie Gervais Danone | Process for producing infant formula products and dairy products |
WO2018028764A1 (en) | 2016-08-08 | 2018-02-15 | Compagnie Gervais Danone | Process for producing infant formula products and acidic dairy products |
CN112423596B (en) * | 2018-07-03 | 2024-04-26 | 美丽生活有限责任公司 | Production and separation of milk fractions using forward osmosis |
EP3955745A4 (en) * | 2019-04-18 | 2023-01-18 | Fonterra Co-Operative Group Limited | Dairy product and process |
RU2717971C1 (en) * | 2019-07-05 | 2020-03-27 | Общество с ограниченной ответственностью «СТМЕМБ» | Method for producing dry whey product |
WO2021013489A1 (en) * | 2019-07-24 | 2021-01-28 | Tetra Laval Holdings & Finance S.A. | Plant and method for concentrating a substance in a milk product |
BE1027671B1 (en) * | 2019-08-12 | 2021-05-10 | Anheuser Busch Inbev Sa | POWDERED PROTEIN COMPOSITION |
BR112022025567A2 (en) | 2020-06-15 | 2023-03-07 | Building Block Nutritionals Llc | NUTRITIONAL FORMULA |
CN114304369A (en) * | 2020-09-29 | 2022-04-12 | 内蒙古伊利实业集团股份有限公司 | Whey protein composition and preparation method and application thereof |
CN115590204A (en) * | 2022-11-02 | 2023-01-13 | 益森益美健康科技(北京)有限公司(Cn) | Composition for enhancing anti-aging of mammals |
Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5085874A (en) * | 1988-03-28 | 1992-02-04 | Hans Jungvid Aktiebolag | Feeding-stuff |
JPH04228026A (en) * | 1990-05-22 | 1992-08-18 | Abbott Lab | Prepared milk and preparation thereof |
US5169666A (en) * | 1991-11-14 | 1992-12-08 | The United States Of America As Represented By The Secretary Of Agriculture | Preparation of simulated human milk protein by low temperature microfiltration |
WO1996008155A1 (en) * | 1994-09-16 | 1996-03-21 | New Zealand Dairy Board | Physical separation of casein and whey proteins |
JPH1070992A (en) * | 1996-08-30 | 1998-03-17 | Suntory Ltd | Production of oil and fat containing unsaturated fatty acid |
JP2000060424A (en) * | 1998-08-19 | 2000-02-29 | Meiji Milk Prod Co Ltd | Infant food composition adjusted with phospholipid and fatty acid composition |
JP2001029010A (en) * | 1999-07-26 | 2001-02-06 | Snow Brand Milk Prod Co Ltd | Nutrient composition |
JP2005514017A (en) * | 2001-12-21 | 2005-05-19 | ワイス | Compositions for infant formulas containing large amounts of alpha-lactalbumin |
WO2008067486A2 (en) * | 2006-11-29 | 2008-06-05 | Prolacta Bioscience, Inc. | Human milk compositions and methods of making and using same |
JP2009514511A (en) * | 2005-11-04 | 2009-04-09 | アルラ フーズ アンバ | Concentrated natural sialyl lactose, concentrate derived from dairy products, and preparation method thereof |
WO2009068549A1 (en) * | 2007-11-26 | 2009-06-04 | Nestec S.A. | Age-tailored nutrition system for infants |
Family Cites Families (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4309417A (en) * | 1980-07-10 | 1982-01-05 | Stauffer Chemical Company | Protein fortified isotonic beverages |
NZ240725A (en) | 1990-11-30 | 1994-05-26 | Snow Brand Milk Products Co Ltd | Preparation of milk having a high alpha-lactalbumin content by ultrafiltration or cross-flow filtration treatment of heat treated milk |
WO1994013148A1 (en) | 1992-12-11 | 1994-06-23 | Immunotec Research Corporation Ltd. | Process for producing an undernatured whey protein concentrate |
DE69919019T2 (en) | 1998-11-24 | 2004-11-25 | Société des Produits Nestlé S.A. | Process for the preparation of a protein composition and a baby food containing the same |
GB9923048D0 (en) * | 1999-09-29 | 1999-12-01 | Nestle Sa | Composition comprising casein protein and whey protein |
WO2001003515A1 (en) * | 1999-07-07 | 2001-01-18 | New Zealand Co-Operative Dairy Company Limited | Method of obtaining protein isolates and concentrates from colostrum |
US6623781B2 (en) | 1999-07-26 | 2003-09-23 | Cornell Research Foundation, Inc. | Microfiltration of skim milk for cheese making and whey proteins |
FI115752B (en) * | 2002-05-14 | 2005-07-15 | Valio Oy | A process for use in the manufacture of a milk product having a low lactose or lactose content |
US7169428B2 (en) | 2002-08-27 | 2007-01-30 | Select Milk Producers Inc. | Dairy compositions and method of making |
US20050181095A1 (en) * | 2004-02-18 | 2005-08-18 | Dominion Nutrition, Inc. | Concentrated-protein food product and process |
US20080206415A1 (en) * | 2004-10-07 | 2008-08-28 | Next Proteins, Inc. | Protein beverage and method of making the same |
WO2006058083A2 (en) | 2004-11-24 | 2006-06-01 | Cornell Research Foundation, Inc. | Protein and calcium fortification system for clear and opaque beverages |
DE102005050879A1 (en) * | 2005-10-21 | 2006-03-23 | Schubert Holding Ag & Co. Kg | Use of powdered mixtures or vegetable or animal protein mixture (obtained by quellung) as food additives for applying in finished or in the preparation of food and/or beverages |
US8889208B2 (en) * | 2005-11-09 | 2014-11-18 | Wisconsin Alumni Research Foundation | Purification of beta casein from milk |
US20070134396A1 (en) * | 2005-12-13 | 2007-06-14 | Kraft Foods Holding, Inc. | Modified Whey Protein For Low Casein Processed Cheese |
WO2007076873A1 (en) | 2006-01-05 | 2007-07-12 | Arla Foods Amba | Low-carbohydrate milk with original calcium |
US20070280997A1 (en) * | 2006-05-31 | 2007-12-06 | Pacifichealth Laboratories, Inc. | Composition for enhancing muscle recovery |
CN101194652A (en) * | 2006-12-05 | 2008-06-11 | 上海光明奶酪黄油有限公司 | Remade cheese and method for producing the same |
BRPI0807230B1 (en) * | 2007-02-02 | 2018-11-06 | Arla Foods Amba | drinkable yogurt, and its manufacturing process |
WO2009011573A1 (en) | 2007-07-18 | 2009-01-22 | Campina Nederland Holding B.V. | Heat stable nutritional beverage and method of preparing it |
LT5581B (en) * | 2007-11-10 | 2009-07-27 | Vytautas FEDARAVIČIUS | Process for producing milk product with higher l-arginine content |
CN101491287B (en) * | 2008-01-24 | 2012-05-23 | 滕国新 | Method for extracting lactose and whey protein from whey |
MX2012004738A (en) | 2009-10-28 | 2012-05-23 | Valio Ltd | Whey protein product and a method for its preparation. |
FI124323B (en) | 2011-02-18 | 2014-06-30 | Valio Oy | Milk-based product and process for its preparation |
-
2010
- 2010-10-25 MX MX2012004738A patent/MX2012004738A/en active IP Right Grant
- 2010-10-25 BR BR112012009744-0A patent/BR112012009744B1/en active IP Right Grant
- 2010-10-25 ES ES10781921T patent/ES2852749T3/en active Active
- 2010-10-25 CN CN2010800487332A patent/CN102595915A/en active Pending
- 2010-10-25 CN CN201710867198.7A patent/CN107646976A/en active Pending
- 2010-10-25 PL PL10781921T patent/PL2493325T3/en unknown
- 2010-10-25 LT LTEP10781921.1T patent/LT2493325T/en unknown
- 2010-10-25 EP EP10781921.1A patent/EP2493325B1/en not_active Revoked
- 2010-10-25 DK DK10781921.1T patent/DK2493325T3/en active
- 2010-10-25 KR KR1020127013565A patent/KR20120098753A/en not_active Application Discontinuation
- 2010-10-25 WO PCT/FI2010/050843 patent/WO2011051557A1/en active Application Filing
- 2010-10-25 JP JP2012535891A patent/JP2013509171A/en active Pending
- 2010-10-25 AU AU2010311316A patent/AU2010311316B2/en active Active
- 2010-10-25 CA CA2778360A patent/CA2778360A1/en not_active Abandoned
- 2010-10-26 AR ARP100103928A patent/AR078779A1/en active IP Right Grant
-
2012
- 2012-04-24 IL IL219403A patent/IL219403A/en active IP Right Grant
-
2015
- 2015-07-01 JP JP2015132362A patent/JP6509058B2/en active Active
Patent Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5085874A (en) * | 1988-03-28 | 1992-02-04 | Hans Jungvid Aktiebolag | Feeding-stuff |
JPH04228026A (en) * | 1990-05-22 | 1992-08-18 | Abbott Lab | Prepared milk and preparation thereof |
US5169666A (en) * | 1991-11-14 | 1992-12-08 | The United States Of America As Represented By The Secretary Of Agriculture | Preparation of simulated human milk protein by low temperature microfiltration |
WO1996008155A1 (en) * | 1994-09-16 | 1996-03-21 | New Zealand Dairy Board | Physical separation of casein and whey proteins |
JPH1070992A (en) * | 1996-08-30 | 1998-03-17 | Suntory Ltd | Production of oil and fat containing unsaturated fatty acid |
JP2000060424A (en) * | 1998-08-19 | 2000-02-29 | Meiji Milk Prod Co Ltd | Infant food composition adjusted with phospholipid and fatty acid composition |
JP2001029010A (en) * | 1999-07-26 | 2001-02-06 | Snow Brand Milk Prod Co Ltd | Nutrient composition |
JP2005514017A (en) * | 2001-12-21 | 2005-05-19 | ワイス | Compositions for infant formulas containing large amounts of alpha-lactalbumin |
JP2009514511A (en) * | 2005-11-04 | 2009-04-09 | アルラ フーズ アンバ | Concentrated natural sialyl lactose, concentrate derived from dairy products, and preparation method thereof |
WO2008067486A2 (en) * | 2006-11-29 | 2008-06-05 | Prolacta Bioscience, Inc. | Human milk compositions and methods of making and using same |
WO2009068549A1 (en) * | 2007-11-26 | 2009-06-04 | Nestec S.A. | Age-tailored nutrition system for infants |
Also Published As
Publication number | Publication date |
---|---|
KR20120098753A (en) | 2012-09-05 |
EP2493325B1 (en) | 2020-12-02 |
AR078779A1 (en) | 2011-11-30 |
CN102595915A (en) | 2012-07-18 |
AU2010311316B2 (en) | 2015-03-12 |
LT2493325T (en) | 2021-04-26 |
PL2493325T3 (en) | 2021-06-28 |
DK2493325T3 (en) | 2021-02-15 |
BR112012009744B1 (en) | 2018-04-03 |
EP2493325A1 (en) | 2012-09-05 |
IL219403A0 (en) | 2012-06-28 |
JP6509058B2 (en) | 2019-05-08 |
WO2011051557A1 (en) | 2011-05-05 |
AU2010311316A1 (en) | 2012-05-31 |
MX2012004738A (en) | 2012-05-23 |
BR112012009744A2 (en) | 2015-09-01 |
ES2852749T3 (en) | 2021-09-14 |
IL219403A (en) | 2017-06-29 |
RU2012121886A (en) | 2013-12-10 |
JP2013509171A (en) | 2013-03-14 |
CN107646976A (en) | 2018-02-02 |
CA2778360A1 (en) | 2011-05-05 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US10993454B2 (en) | Milk-based product and a method for its preparation | |
JP6509058B2 (en) | Whey protein product and method for preparing the same | |
US20120232023A1 (en) | Whey protein product and a method for its preparation | |
JP6693807B2 (en) | Dairy products and methods of preparation | |
JP5027286B2 (en) | Process for producing lactose-free dairy products | |
WO2018028764A1 (en) | Process for producing infant formula products and acidic dairy products | |
FI122675B (en) | Whey protein product and a method for its preparation | |
RU2575610C2 (en) | Product containing milk whey protein and such product manufacture method | |
CN116725195A (en) | Whey protein product and method for preparing same |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20160705 |
|
A601 | Written request for extension of time |
Free format text: JAPANESE INTERMEDIATE CODE: A601 Effective date: 20161004 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20161122 |
|
A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 20170404 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20170714 |
|
A911 | Transfer to examiner for re-examination before appeal (zenchi) |
Free format text: JAPANESE INTERMEDIATE CODE: A911 Effective date: 20170724 |
|
A912 | Re-examination (zenchi) completed and case transferred to appeal board |
Free format text: JAPANESE INTERMEDIATE CODE: A912 Effective date: 20170901 |
|
A601 | Written request for extension of time |
Free format text: JAPANESE INTERMEDIATE CODE: A601 Effective date: 20180918 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20181005 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20190402 |
|
R150 | Certificate of patent or registration of utility model |
Ref document number: 6509058 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |